US2381855A - Raw material for resin synthesis - Google Patents
Raw material for resin synthesis Download PDFInfo
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- US2381855A US2381855A US454077A US45407742A US2381855A US 2381855 A US2381855 A US 2381855A US 454077 A US454077 A US 454077A US 45407742 A US45407742 A US 45407742A US 2381855 A US2381855 A US 2381855A
- Authority
- US
- United States
- Prior art keywords
- pentaerythritol
- calcium
- raw material
- lime
- rosin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229920005989 resin Polymers 0.000 title description 19
- 239000011347 resin Substances 0.000 title description 19
- 239000002994 raw material Substances 0.000 title description 9
- 230000015572 biosynthetic process Effects 0.000 title description 2
- 238000003786 synthesis reaction Methods 0.000 title 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 27
- 238000000034 method Methods 0.000 description 20
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 18
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 18
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 16
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 13
- 235000011941 Tilia x europaea Nutrition 0.000 description 13
- 239000004571 lime Substances 0.000 description 13
- 239000000243 solution Substances 0.000 description 13
- CBOCVOKPQGJKKJ-UHFFFAOYSA-L Calcium formate Chemical compound [Ca+2].[O-]C=O.[O-]C=O CBOCVOKPQGJKKJ-UHFFFAOYSA-L 0.000 description 12
- 239000004281 calcium formate Substances 0.000 description 12
- 235000019255 calcium formate Nutrition 0.000 description 12
- 229940044172 calcium formate Drugs 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- 239000007787 solid Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 11
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 10
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 10
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 9
- 235000019253 formic acid Nutrition 0.000 description 9
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 8
- 239000002253 acid Substances 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 7
- 229910052791 calcium Inorganic materials 0.000 description 7
- 239000011575 calcium Substances 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002966 varnish Substances 0.000 description 5
- 239000004280 Sodium formate Substances 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 235000019260 propionic acid Nutrition 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 4
- 235000019254 sodium formate Nutrition 0.000 description 4
- 235000011054 acetic acid Nutrition 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 3
- 229940044600 maleic anhydride Drugs 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000003472 neutralizing effect Effects 0.000 description 3
- 229940032330 sulfuric acid Drugs 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 150000001243 acetic acids Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- DWPDSISGRAWLLV-JHZYRPMRSA-L calcium;(1r,4ar,4br,10ar)-1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylate Chemical compound [Ca+2].C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C([O-])=O.C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C([O-])=O DWPDSISGRAWLLV-JHZYRPMRSA-L 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 150000004674 formic acids Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 150000004672 propanoic acids Chemical class 0.000 description 2
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 241000585703 Adelphia <angiosperm> Species 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000002036 drum drying Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000001640 fractional crystallisation Methods 0.000 description 1
- 235000010985 glycerol esters of wood rosin Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 235000021388 linseed oil Nutrition 0.000 description 1
- 239000000944 linseed oil Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
- C09F1/00—Obtaining purification, or chemical modification of natural resins, e.g. oleo-resins
Definitions
- This invention relates to the production of raw materials suitable for the preparation of synthetic resins. It relates to the production of a new raw material, containing pentaerythritol and calcium formate, which, when reacted with rosin, yields resins which are clear and homogeneous in appearance and completely soluble in the vege-' table oils customarily used in varnish-making.
- pentaerythritol is used to cover all of the organic products .of the reaction. After the completion .of the above reaction, it has been customaryto add sulfuricacid to the mixture to effect precipitation of the calcium as' the relatively insoluble sulfate, liberating the formic acid. The strongly acid solution is then evaporated and hyde in the presence of of impurities such as calcium sulfate or sodium formate.
- the present invention provides a method of producing a new rawmaterialwhich may-be used in conjunction with rosin to yield resins which are free from turbidity themselves and which can be used in the preparation of clear homogeneous varnishes. This method also gives a higher yield of the pentaerythritol and avoids the expense of the crystallizations formerly necessary to produce a raw material of satisfactory purity.
- the method comprises reacting an aqueous solution of.
- a The preferred procedure comprises reacting a. solution of about 4.
- the product obtained contains substantially all of the pentaerythritol and organic by-products obtained in the reaction and at least part of the calcium formate.
- the yield of useful compounds obtained is 85-95% the pentaerythritol isisolated by crystallization.
- Another method involves addition of sodium carbonate, which precipitates calcium carbonate and leaves sodium formate in solution. The solution is then concentrated and the pentaerythritol is separated from the sodium formate by-fractional crystallization.
- Pentaerythritol hasbeensuggested as a raw material in the preparation of oil-soluble synthetic resins suitable for use in varnish making.
- the pentaerythritol may be used in .place of some or all ofthe glycerine normally used in thepreparatlon of esterified rosin, known in the varnish industryas ester gum? .
- the resins may be further hardened by the use'of maleicanhydride or maleic acid.
- the pentaerythritol prepared as above noted tends to produce turbid resins, which in turn give turbid it has been-found that Y of theory, compared with -75% by previous methods.
- the product obtained. can be used directly in the preparation of rosin modified resins or may be further concentrated before being used in the formation of resins.
- this material containing for the most part calcium formate and pentaerythritol, will react readily with rosin to produce clear resins.
- the calcium formats which' is present apparently reacts with the high boiling acids of the rosin to form calcium abietate or limed rosin as it is better known in the trade.
- the pentaerythritolintum serves to esterify the rosin acidsand produce a clear homogeneous resin of high-melting point. Any calciumsalts of acetic or propionic'acids which may be present will react in a manner similar to calcium formate.
- the formic acid evolved in the preparation of the resins may be recovered.
- the proportion of calcium formate to pentaerythritol in the product may be altered over a wide range to suit the requirements of the typeof resin to be made from it.
- the solution is filtered while hot to remove the insoluble matter in the lime, and the resulting solution used in this state or after concentration without removal of any calcium formate. This procedure gives a product which contains 30-35% calcium formate based on the total solids.
- the solution is concentrated, preferably under reduced pressure to prevent discoloration, and is then filtered at a temperature of 90 to 110 C. to remove solids consisting chiefly of calcium iormate.
- a temperature of 90 to 110 C. to remove solids consisting chiefly of calcium iormate.
- other methods of separating the solids from the liquid may be employed, such as centrifuging, etc.
- Calcium fox-mate is almost as soluble at room temperature as at 100 C. (16 grams per 100 grams of water at C., and 18 grams per 100 grams at 100 C.) while the solubility of pentaerythritol increases rapidly with temperature (6.27 grams per 100 grams at. 20 C., and 98 grams per 100 grams at 100 C.).
- acetaldehyde and formaldehyde 1
- the usual proportions of reactants and water used give a product containing 20-40% total solids.
- This product can be concentrated and filtered at about 100 C. to give a filtrate containing 50 to 60% solids without much loss of pentaerythritol in the filter cake.
- the filter cake can be washed with water to recover pentaerythritol whereupon the washings may be returned to the next batch for concentration so that practically no loss of pentaerythritol and the other useful by-product occurs.
- the calcium formate content of the prodnot is thereby varied over the range of to 12% number and amounts of the chemicals required are also reduced and the process of working up the products is simplified by the elimination of the crystallization of the product, all of which represents considerable economy in manufacture.
- Example 1 Twenty-four hundred grams of water and 182 grams (2.32 mols) of 94% lime were placed in a 5-liter 3-necked flask, equipped with thermometer, stirring device and dropping funnel. While the contents of the flask were being stirred, 16.6 mols of formaldehyde, as a 37% solution, was added. The mixture was quickly'warmed to 30 C.,' and'4 mols of acetaldehyde was added at a constant rate over a period of minutes. The tip of the funnel through which the acetaldehyde was added extended below the surface of the mixture. During the first 10 minutes of the addition of the acetaldehyde, the temperature rose to 42 C.
- the filtrate on cooling to room temperature becomes a slurry containing pentaerythritol crystals and maybe used in this form for the preparation of resins or may be further dried to produce a solid product by various well-known means such as spray drying or drum drying.
- the method of reacting the formaldehyde and acetaldehyde in the presence of lime may be varied without departing from the spirit of the invention.
- the main and novel steps of the invention' are the neutralization of the remaining free lime with formic, acetic or propionic acids to stop the progress of the reaction, and the recovery of a product containing varying amounts of calcium formate by evaporation and filtration of the hot liquor.
- the amount of the acids which is required is very small inasmuch as most of the lime is already neutralized by-the formic acid produced in the reaction, as shown in the equation above.
- the inorganic substances left in the reaction mixture are compatible with the resin, while the previous processes left insoluble substances such as calcium sulfate and sodium formate in-the reaction mixture.
- Emmple 3 s,ss1,ass' v m1 suitable for the preparation of rosin-modified therefrom.
- the resultant solution was then cooled to 10 (2., during which crystallization took place.
- the solids were separated from theliquid and were found to be 97% pentaerythritol and 3% calcium Iormate.
- the yield of pentaerythritol was 74% of theory.
- Example 4 To a molten adduct of 100 parts by weight of rosinand 3.96 parts tected by an atmosphere of CO2, were added 7.0 parts of glycerine and 7.25 parts of the raw material containing 97% of pentaerythritol as prepared in Example 3. The mixture was heated to 275-280 C. and held at this 4% hours, at which time the acid number had iallen to 14. The resin, which had a melting point of 105 C., was clear and exceptionally'light in color, W W on the customary rosin scale, and produced an especially fast-drying varnish when cooked into oil.
- this application relates to the preparation of a raw material containing pentaerythri- 25 water reduced the con-.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Phenolic Resins Or Amino Resins (AREA)
Description
patents lent ofa polyvalent metal.
Patented Aug. 7, 1945 Le Roy U. Spence, Elkins Park,
and Charles 11.
McKeever, Philadelphia, Pa., assignors to The Besinous Products & Chemical Company, Phil adelphia, Pa., a corporation of Delaware No Drawing. Application August 7, 1942,
Serial No. 454,077
2 Claims. 21. 260-637 This invention relates to the production of raw materials suitable for the preparation of synthetic resins. It relates to the production of a new raw material, containing pentaerythritol and calcium formate, which, when reacted with rosin, yields resins which are clear and homogeneous in appearance and completely soluble in the vege-' table oils customarily used in varnish-making.
It is well known that formaldehyde and acetaldehyde react, under the catalytic eifect'of alkaline materials such as lime, to form 'pentaerythritol and other by products, including sugars.
Several modified processes have been developed for conducting this reaction, and the effect of suchfactors as time and temperature of reaction, concentration of' reactants and modifying agents have been studied and disclosed in such as U. S. 1,678,623, 1,716,110, 2,152,371, 2,170,624, 2,186,272, 2,206,379, 2,223,421 and 2,240,-
734. The main reaction which takes place in an alkaline medium is usually represented by the following equation:
in which M is amonovalentmetal or the equiva- It is known that many side-reactions may occur with the production of a mixture of by-products as well as pentaerythritol, but in the discussion which follows,
the term pentaerythritol is used to cover all of the organic products .of the reaction. After the completion .of the above reaction, it has been customaryto add sulfuricacid to the mixture to effect precipitation of the calcium as' the relatively insoluble sulfate, liberating the formic acid. The strongly acid solution is then evaporated and hyde in the presence of of impurities such as calcium sulfate or sodium formate.
The present invention provides a method of producing a new rawmaterialwhich may-be used in conjunction with rosin to yield resins which are free from turbidity themselves and which can be used in the preparation of clear homogeneous varnishes. This method also gives a higher yield of the pentaerythritol and avoids the expense of the crystallizations formerly necessary to produce a raw material of satisfactory purity. The method comprises reacting an aqueous solution of.
formaldehyde and acetaldehyde in the presence of lime until the aldehyde content has fallen to less than 4%, neutralizing the reaction mixture with formic, acetic, or propionic acid until a pH of about 5.5 to about 6.5 is reached, separating any insoluble extraneous matter, and concentrating the desired product. a The preferred procedure comprises reacting a. solution of about 4.
to 5 mols of formaldehyde and 1 mol of acetaldeabout .5 to .7 mol of lime at a temperature of 45 'C. for about two hours or until the aldehyde content of the mixture has fallen to about 2 to 4%. Thereafter, the remaining small amount oflime in the mixture is neutralized with formic acid, acetic acid or, propionic acid (as contrasted with sulfuric acid used in previous processes). The product obtained contains substantially all of the pentaerythritol and organic by-products obtained in the reaction and at least part of the calcium formate. In this way,
- the yield of useful compounds obtained is 85-95% the pentaerythritol isisolated by crystallization.
Another method involves addition of sodium carbonate, which precipitates calcium carbonate and leaves sodium formate in solution. The solution is then concentrated and the pentaerythritol is separated from the sodium formate by-fractional crystallization.
Pentaerythritol hasbeensuggested as a raw material in the preparation of oil-soluble synthetic resins suitable for use in varnish making. The pentaerythritol may be used in .place of some or all ofthe glycerine normally used in thepreparatlon of esterified rosin, known in the varnish industryas ester gum? .The resins may be further hardened by the use'of maleicanhydride or maleic acid. However, the pentaerythritol prepared as above noted tends to produce turbid resins, which in turn give turbid it has been-found that Y of theory, compared with -75% by previous methods.
The product obtained. can be used directly in the preparation of rosin modified resins or may be further concentrated before being used in the formation of resins. In contrast to the pentaerythritol prepared by using sulfuric acid to neutrallze the lime, this material, containing for the most part calcium formate and pentaerythritol, will react readily with rosin to produce clear resins. The calcium formats which' is present apparently reacts with the high boiling acids of the rosin to form calcium abietate or limed rosin as it is better known in the trade. The pentaerythritolintum serves to esterify the rosin acidsand produce a clear homogeneous resin of high-melting point. Any calciumsalts of acetic or propionic'acids which may be present will react in a manner similar to calcium formate. The formic acid evolved in the preparation of the resins may be recovered.
The proportion of calcium formate to pentaerythritol in the product may be altered over a wide range to suit the requirements of the typeof resin to be made from it. After the acidification of the pentaerythritol reaction mixture, the solution is filtered while hot to remove the insoluble matter in the lime, and the resulting solution used in this state or after concentration without removal of any calcium formate. This procedure gives a product which contains 30-35% calcium formate based on the total solids.
If removal of part of'the calcium formate is desired, the solution is concentrated, preferably under reduced pressure to prevent discoloration, and is then filtered at a temperature of 90 to 110 C. to remove solids consisting chiefly of calcium iormate. Obviously, other methods of separating the solids from the liquid may be employed, such as centrifuging, etc. Calcium fox-mate is almost as soluble at room temperature as at 100 C. (16 grams per 100 grams of water at C., and 18 grams per 100 grams at 100 C.) while the solubility of pentaerythritol increases rapidly with temperature (6.27 grams per 100 grams at. 20 C., and 98 grams per 100 grams at 100 C.). In the condensation of acetaldehyde and formaldehyde, 1
the usual proportions of reactants and water used givea product containing 20-40% total solids. This product can be concentrated and filtered at about 100 C. to give a filtrate containing 50 to 60% solids without much loss of pentaerythritol in the filter cake. The filter cake can be washed with water to recover pentaerythritol whereupon the washings may be returned to the next batch for concentration so that practically no loss of pentaerythritol and the other useful by-product occurs. The calcium formate content of the prodnot is thereby varied over the range of to 12% number and amounts of the chemicals required are also reduced and the process of working up the products is simplified by the elimination of the crystallization of the product, all of which represents considerable economy in manufacture.
The following examples serve to illustrate this invention:
Example 1 Twenty-four hundred grams of water and 182 grams (2.32 mols) of 94% lime were placed in a 5-liter 3-necked flask, equipped with thermometer, stirring device and dropping funnel. While the contents of the flask were being stirred, 16.6 mols of formaldehyde, as a 37% solution, was added. The mixture was quickly'warmed to 30 C.,' and'4 mols of acetaldehyde was added at a constant rate over a period of minutes. The tip of the funnel through which the acetaldehyde was added extended below the surface of the mixture. During the first 10 minutes of the addition of the acetaldehyde, the temperature rose to 42 C. due to the exothermic nature of the reaction, and thereafter the temperature was maintained at 40-44 C. After all of the acetaldehyde had been added, the mixture was held at 40-44" C. and stirred for one hour. At this point, about 98% of the aldehydes had condensed as shown by 0 analyses for the remaining aldehydes by the method of Adams 8: Adkins (J. A. C. S. 47, 1938). Thirty cc. of formic acid, in solution, was then added until a pH of 5.5-6.5 was reached.
. The solution was filtered, evaporated to a weight of the total solids. For example, the following table indicates the results obtained at various concentrations of the filtrate:
The filtrate on cooling to room temperature becomes a slurry containing pentaerythritol crystals and maybe used in this form for the preparation of resins or may be further dried to produce a solid product by various well-known means such as spray drying or drum drying.
The method of reacting the formaldehyde and acetaldehyde in the presence of lime may be varied without departing from the spirit of the invention. The main and novel steps of the invention'are the neutralization of the remaining free lime with formic, acetic or propionic acids to stop the progress of the reaction, and the recovery of a product containing varying amounts of calcium formate by evaporation and filtration of the hot liquor. The amount of the acids which is required is very small inasmuch as most of the lime is already neutralized by-the formic acid produced in the reaction, as shown in the equation above. Also, as emphasized above, the inorganic substances left in the reaction mixture are compatible with the resin, while the previous processes left insoluble substances such as calcium sulfate and sodium formate in-the reaction mixture. The
of 1800 grams under reduced pressure, then heated ,to C. and the solids separated as rapidly as possible at this temperature.
The remaining solution was analyzed for alcium by the standard oxalate method, and the results converted to equivalents of calcium formate. Total solids were determined by the Carl Fischer method. The amount of pentaerythritol was calculated by difference. The analysis showed: 45.3% total solids, of which 8.9% was calcium formats and 36.4% pentaerythritol. This was equivalent to a 02% yield.
To a molten adduct 01 parts by weight of rosin and 3.63 parts of maleic anhydride were added 4.63 parts of glycerine and 22.6 parts oi the raw material obtained in Example 1 above. The water was evaporated from this mixture by heat, and the remaining resinous mass was then beated to 275-280 C. and held at this temperature until the acid number had fallen to 17. During the course of the heating, part of the formic acid, liberated from the calcium formate by action of abietic and other rosin acids, was decomposed and escaped as carbon monoxide while the balance distilled ofi unchanged. The-carbon monoxide served in part to blanket the surface of the resin and prevent oxidation, which ordinarily causes poor color in the resin. The resin was poured out and cooled. It was found to have a melting point of C.', as determined by the capillary tube method, and was entirely clear.
A varnish, of 50% solids content, prepared by cooking 100 pounds of this resin in 25 gallons of bodied linseed oil (viscosity Z4 on Gardner-Holdt scale) had excellent propertie such as clarity, dryingrate, and chemical resistance.
Emmple 3 s,ss1,ass' v m1 suitable for the preparation of rosin-modified therefrom. The resultant solution was then cooled to 10 (2., during which crystallization took place. The solids were separated from theliquid and were found to be 97% pentaerythritol and 3% calcium Iormate. One wash 0! the solids with half their weight oi cold tent of calcium formats to less than 1%. The yield of pentaerythritol was 74% of theory.
Example 4 To a molten adduct of 100 parts by weight of rosinand 3.96 parts tected by an atmosphere of CO2, were added 7.0 parts of glycerine and 7.25 parts of the raw material containing 97% of pentaerythritol as prepared in Example 3. The mixture was heated to 275-280 C. and held at this 4% hours, at which time the acid number had iallen to 14. The resin, which had a melting point of 105 C., was clear and exceptionally'light in color, W W on the customary rosin scale, and produced an especially fast-drying varnish when cooked into oil.
Whereas this application relates to the preparation of a raw material containing pentaerythri- 25 water reduced the con-.
of maleic anhydride, protemperature forsynthetic resins, application Serial No. 454,076,
filed simultaneously, claims the process of preparing pure pentaerythritol from this raw material.
We claim;
1. In the process of by the condensation in aqueous solution of about four mols of formaldehyde and about one mol of acetaldehyde in the presence oi about 0.6 mol of lime until the aldehyde content of the mixture is about 2% to 4%. the improvement which comprises the step of neutralizing the lime, after said condensation, with an acid from the group consisting of formic, acetic, and propionic acids.
2. In the process oi. preparing pentaerythritol by the condensation inaqueous solution of about four mols of formaldehyde and about one moi of acetaldehyde in the presence of about 0.6 mol of lime. until the aldehyde content of the mixture is about 2% to 4%, the improvement which comprises the step of neutralizing the lime, after said condensation. with formic acid.
LE ROY U. SPENCE. CHARLES H; Mom.
preparing pentaerythrltol
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US454077A US2381855A (en) | 1942-08-07 | 1942-08-07 | Raw material for resin synthesis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US454077A US2381855A (en) | 1942-08-07 | 1942-08-07 | Raw material for resin synthesis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2381855A true US2381855A (en) | 1945-08-07 |
Family
ID=23803209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US454077A Expired - Lifetime US2381855A (en) | 1942-08-07 | 1942-08-07 | Raw material for resin synthesis |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2381855A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2486774A (en) * | 1946-03-01 | 1949-11-01 | Trojan Powder Co | Process for the preparation of pentaerythritol |
| US2837468A (en) * | 1955-12-23 | 1958-06-03 | Trojan Powder Co | Purification of polyhydric alcohols |
-
1942
- 1942-08-07 US US454077A patent/US2381855A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2486774A (en) * | 1946-03-01 | 1949-11-01 | Trojan Powder Co | Process for the preparation of pentaerythritol |
| US2837468A (en) * | 1955-12-23 | 1958-06-03 | Trojan Powder Co | Purification of polyhydric alcohols |
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